CN212320479U - Indirect evaporative fluid cooling device with built-in heat exchanger - Google Patents
Indirect evaporative fluid cooling device with built-in heat exchanger Download PDFInfo
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- CN212320479U CN212320479U CN202020801064.2U CN202020801064U CN212320479U CN 212320479 U CN212320479 U CN 212320479U CN 202020801064 U CN202020801064 U CN 202020801064U CN 212320479 U CN212320479 U CN 212320479U
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Abstract
The utility model relates to an indirect evaporation fluid cooling device of built-in heat exchanger contains shell, income wind gap, air outlet, fan, fluid entry, receives the water module, sprays module, evaporative cooling heat exchanger, fluid outlet, wet membrane, heat exchanger, catch basin, circulating water pump, moisturizing valve. The cooling efficiency and the refrigerating capacity of the whole device are greatly improved by organically combining the cold water generated by the humidifying wet film and the evaporative cooling heat exchanger after being heated.
Description
Technical Field
The utility model relates to an application scenario at central air conditioning system place, in particular to air conditioner is energy-conserving and natural cooling field.
Background
At present, the conventional cooling tower mainly adopts an open tower, the water consumption is high, and the temperature of outlet water is higher than the temperature of external air wet bulb, and is generally higher than the temperature of the wet bulb by 2-5 ℃. The conventional closed cooling tower has the advantages of cleanness, water saving, energy saving, capability of directly supplying cold to the tail end, capability of cooling various fluid media and the like, but also has the defects of high cost, large volume, heaviness and the like. The defects are that the tube type heat exchanger used by the conventional closed cooling tower has low efficiency, the surface area is not large enough, water spraying is uneven, and cold water prepared in the evaporative cooling process is directly sprayed on the tube type evaporative cooling heat exchanger, so that the water temperature and the water evaporation capacity of the evaporative heat exchange tube are reduced, the cold energy of the cold water generated by evaporative cooling is wasted, and the cooling efficiency and the refrigerating capacity of the conventional closed cooling tower are reduced.
Disclosure of Invention
In order to solve the technical problem that conventional closed cooling tower cooling efficiency is low refrigeration ability is not high, the embodiment of the utility model provides an adopt the cold water that produces with the wet membrane of humidification to pass through the heat exchanger to being cooled off by cooling fluid, spray on the evaporation cooling heat exchanger after the cold water that the wet membrane produced is heated simultaneously, both combine organically to have increased substantially the cooling efficiency and the refrigeration ability of whole device together.
The utility model discloses the technical scheme of implementation case as follows:
an indirect evaporative fluid cooling device with a built-in heat exchanger is characterized in that:
comprises a shell, an air inlet, an air outlet, a fan, a fluid inlet, a water collecting module, a spraying module, an evaporative cooling heat exchanger, a fluid outlet, a wet film, a heat exchanger, a water collecting tank, a circulating water pump and a water replenishing valve;
the fan is arranged at the upper part of the indirect evaporative fluid cooling device, the water receiving module is arranged below the fan, the evaporative cooling heat exchanger is arranged below the water receiving module, the wet film is arranged below the evaporative cooling heat exchanger, and the wet film is communicated with the air inlet;
the fluid inlet, the evaporative cooling heat exchanger, the heat exchanger and the fluid outlet are connected in sequence through a cooled fluid pipeline;
the spray module is arranged above the evaporative cooling heat exchanger, a plurality of spray heads of the spray module are uniformly distributed above the upper surface of the evaporative cooling heat exchanger, and nozzles of the plurality of spray heads are arranged in alignment with the upper surface of the evaporative cooling heat exchanger;
the water replenishing valve is connected with the water collecting tank; the water collecting tank, the circulating water pump, the heat exchanger and the spraying module are connected through a circulating water pipeline.
During operation, the working modes of circulating water, external air and cooled fluid are as follows:
when the circulating water pump operates, circulating water in the water collecting tank firstly enters the heat exchanger through the circulating water pump along the circulating water pipeline and then enters the spraying module; the water is uniformly sprayed on the evaporative cooling heat exchanger through a plurality of spray heads of the spray module; circulating water flowing out of the evaporative cooling heat exchanger flows into the wet film and then flows into the water collecting tank; the circulating water and the cooled fluid exchange heat in the heat exchanger;
when the fan operates, external air enters the wet film from the air inlet to be humidified and cooled; the humidified and cooled external air upwards enters the evaporative cooling heat exchanger for evaporation and heat exchange, then flows through the water receiving module and is sent out by the fan;
when the cooled fluid works, the cooled fluid enters the evaporative cooling heat exchanger through the fluid inlet to perform evaporative cooling heat exchange, then exchanges heat through the heat exchanger, and then flows out through the fluid outlet.
The embodiment of the utility model provides a concrete technological effect as follows:
the utility model discloses the cold water that produces with wet film passes through the heat exchanger and is cooled off by cooling fluid, make whole device by cooling fluid because of its and circulating water between the heat transfer ability strengthen by a wide margin, its leaving water temperature further reduces, be close the circulating water temperature of intaking that gets into the heat exchanger, the cooling capacity of whole device has been increased substantially, the cold water that wet film produced simultaneously sprays on evaporation cooling heat exchanger after being heated, multiplicable system water evaporation capacity, also reach the effect that increases this cooling device cooling capacity, both combine together organically and increased the cooling efficiency and the cooling capacity of whole device by a wide margin.
In another embodiment of the utility model, increased the precooling of air cooling surface cooler to the air, its technical effect as follows:
the utility model uses the air cooling surface cooler to pre-cool the air, the temperature of the cooled air wet bulb is reduced, and then the cold air and the cold water which are lower than the temperature of the external air wet bulb are obtained by the high-efficiency evaporation of the wet film; cooling the cooled fluid by the prepared cold water through a heat exchanger, enabling the wet air which is prepared in the process and is lower than the temperature of the external air wet bulb to enter an evaporative cooling heat exchanger with a water spraying device arranged on the upper part, and cooling the cooled fluid in the evaporative cooling heat exchanger pipe through the cold water and the cold air which are generated in the evaporative cooling process; circulating water heated by the air cooling surface cooler is gradually cooled when flowing out through the evaporative cooling heat exchanger and then flows into the wet film, then cold water with the temperature lower than the wet bulb temperature of the outside air is prepared again and flows into the water collecting tank, and the circulation is carried out. Compare the air and do not have precooling or cold water directly to spray the mode on the evaporation cooling heat exchanger, the utility model discloses an evaporation capacity of evaporation cooling heat exchanger and whole evaporation cooling efficiency all have great promotion to make the cooling capacity of whole device further improve.
Further, the utility model discloses adopt the reposition of redundant personnel to carry out the precooling by cooling fluid to the air in the implementation, can increase system cooling capacity under the dry-cold mode winter, can also preheat the air when the temperature is lower simultaneously, prevent that inside from freezing, do and start the spray pattern winter, increase system cooling capacity, reduce the consumption.
The utility model discloses an in other embodiments, the air precools the surface cooler, sprays module, evaporative cooling heat exchanger, wet film and all is the slope and places for increase corresponding windward area and heat transfer area. The spray heads of the spray modules are uniformly arranged and aligned with the evaporative cooling heat exchanger, and the particle size of sprayed water drops is smaller, so that the evaporative cooling efficiency can be greatly improved; the heat exchanger fins are coated with hydrophilic coatings added with radiation heat dissipation materials for enhancing the heat dissipation effect of heat exchange. These further optimization improvements improve the cooling efficiency and cooling capacity of the entire device.
Drawings
Fig. 1 is a schematic structural view of a fluid cooling device according to a first embodiment of the present invention;
fig. 2 is a schematic view of the installation of the automatic sewage filter device according to the first embodiment of the present invention;
fig. 3 is an installation schematic diagram of an evaporative cooling heat exchanger according to a first embodiment of the present invention;
fig. 4 is a schematic structural view of an evaporative cooling heat exchanger according to a first embodiment of the present invention;
fig. 5 is a schematic structural view of a fluid cooling device according to a second embodiment of the present invention;
fig. 6 is a schematic structural view of a fluid cooling device according to a third embodiment of the present invention;
fig. 7 is a schematic structural view of a fluid cooling device according to a fourth embodiment of the present invention;
110 water receiving module, 110a fluid precooling surface cooler; a 120 evaporative cooling heat exchanger, a 120a evaporative cooling heat exchanger chilled fluid inlet, a 120b evaporative cooling heat exchanger chilled fluid outlet, a 130 air cooled surface air cooler, a 130a air cooled surface air cooler fluid inlet, a 130b air cooled surface air cooler fluid outlet, a 140 air cooled circulation pump, check valve 150; 200 wet film; 300 heat exchanger; 400 of a fan; 510 a catch basin; 520 circulating water pump; 530 automatic filtering and sewage discharging device, 531 check valve, 532 electric valve for sewage discharging and 533 filter screen; 540 spray module; a 550 water replenishing valve; 600 a housing; 710 air intake; 720 air outlet; 810 a fluid inlet; 820 fluid outlet.
Detailed Description
In order to facilitate understanding of the present invention, the present invention will be described more fully hereinafter with reference to the accompanying drawings. The preferred embodiments of the present invention are shown in the drawings. The invention may, however, be embodied in many different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete.
It will be understood that when an element is referred to as being "secured to" another element, it can be directly on the other element or intervening elements may also be present. When an element is referred to as being "connected" to another element, it can be directly connected to the other element or intervening elements may also be present.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. The terminology used in the description of the invention herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention.
The cooled fluid in this embodiment may be water or other liquid medium. In the field of data centers, when a water-cooling air-conditioning system is adopted to cool the data centers, the device can cool chilled water or cooling water of the water-cooling air conditioner. Cooling water is mainly cooled in summer; other seasons mainly cool the chilled water. In the field of data centers, when a liquid cooling air conditioning system is adopted to cool a data center, the device cools cooling liquid of the liquid cooling air conditioning system.
The first embodiment:
the indirect evaporative fluid cooling device of this embodiment, as shown in fig. 1, includes a housing 600, an air inlet 710, an air outlet 720, a fan 400, a fluid inlet 810, a water receiving module 110, a spraying module 540, an evaporative cooling heat exchanger 120, a fluid outlet 820, a wet film 200, a heat exchanger 300, a water collecting tank 510, a circulating water pump 520, and a water replenishing valve 550. The device comprises an air inlet, a wet film, an evaporative cooling heat exchanger, a spraying module, a water receiving module, a fan and an air outlet in sequence from the external air angle; the device comprises a water collecting tank, a circulating water pump, a heat exchanger, a spraying module, an evaporative cooling heat exchanger, a wet film, a water collecting tank and a water replenishing valve in sequence from the circulating water angle; the fluid to be cooled is divided into a fluid inlet, an evaporative cooling heat exchanger, a heat exchanger and a fluid outlet in sequence.
Preferably, an automatic filtering and sewage draining device 530 is further provided between the circulating water pump and the heat exchanger for automatic sewage draining at regular intervals, as shown in fig. 1, and only the installation position of the device is shown in fig. 1.
The automatic filtering and sewage draining device 530 comprises a solenoid valve 1 and a filtering device, and preferably the automatic filtering and sewage draining device 530 comprises a first solenoid valve 531, a filtering device 532, a sewage draining solenoid valve 533, a second solenoid valve 534, a first pipeline 535 and a second pipeline 536. The automatic filtering sewage draining device 530 is required to be matched with the circulating water pump 520, and at least two sets of the automatic filtering sewage draining device 530 and two circulating water pumps 520 are required to be arranged in the whole device, as shown in figure 2. Normal operation is 531,534 open and 533 closed. For cleaning 532a, 533a is open, 531a and 534a are closed, 531b and 534b are open, and 532b is closed. Through such setting for automatic blowdown filter equipment can carry out automatic blowdown with the help of circulating water pump, need not to increase extra dredge pump. In addition, the automatic sewage discharge frequency can be set, and the normal work of the whole device is not influenced while the sewage is discharged.
The fan 400 is arranged in the upper part of the indirect evaporative fluid cooling device, in particular on top of the housing.
The water collecting module 110 is disposed below the blower 400, and is used for collecting water vapor brought out by evaporation of the whole device, and reducing the drift rate of the whole device.
The evaporative cooling heat exchanger 120 is arranged below the water collecting module 110, the wet film 200 is arranged below the evaporative cooling heat exchanger 120, the air cooling surface air cooler 300 is arranged on the front side or below the air inlet direction of the wet film 200, and the air cooling surface air cooler 300 is communicated with the air inlet 710.
The spraying module 540 is disposed above the evaporative cooling heat exchanger 120, a plurality of spray heads of the spraying module 540 are uniformly distributed above the upper surface of the evaporative cooling heat exchanger 120, and nozzles of the plurality of spray heads are disposed in alignment with the upper surface of the evaporative cooling heat exchanger 120.
The water replenishing valve 550 is connected to the sump 510 for replenishing the circulating water.
The physical process that occurs in the heat exchanger 300 is the liquid-to-liquid heat exchange of the cooled fluid with the circulating water from within the sump. For the cooled fluid, the fluid inlet 810, the evaporative cooling heat exchanger 120 and the heat exchanger 300 are sequentially connected, so that the cooled fluid firstly exchanges heat on the heat exchanger through evaporative heat dissipation; for the circulating water, the water collecting tank 510, the circulating water pump 520, the automatic filtering and sewage discharging device 530, the heat exchanger 300 and the spraying module 540 are sequentially connected, so that the circulating water in the water collecting tank exchanges heat with the cooled fluid firstly after being filtered, and the heated circulating water enters the spraying after the heat exchange. The cooled fluid is cooled by adding the heat exchanger and utilizing cold water generated by the wet film, so that the heat exchange between the cooled fluid and the circulating water is greatly enhanced, the temperature of the cooled fluid is closer to the temperature of the water collecting tank, and the current situation that the cooling capacity of the existing closed cooling tower greatly depends on the evaporation and heat dissipation of the circulating water is broken. In addition, the circulating water is also heated by the heat exchanger, so that the evaporation capacity of the circulating water is further improved.
The heat exchanger 300 is disposed in the lower space of the entire apparatus, below the evaporative cooling heat exchanger 120.
Preferably, the heat exchanger 300 is a plate heat exchanger or a shell and tube heat exchanger. Compared with other types of liquid-liquid heat exchangers, the liquid-liquid heat exchanger adopting the plate heat exchanger or shell and tube heat exchanger structure has better heat exchange effect, so that the heat exchanger required under the same refrigerating capacity is smaller in size and weight.
The air inlet 710 is arranged at a position corresponding to the wet film 200 at the lower part of the housing, and the air inlet 710 is directly communicated with the wet film 200.
The indirect evaporative fluid cooling device of the present embodiment operates as follows:
1) the complete fluid cooling cycle process is as follows: the cooled fluid enters the evaporative cooling heat exchanger 120 from the water inlet 810 to be cooled, then flows through the heat exchanger 300 to be cooled for the second time, and then is sent out through the water outlet 820.
2) The complete circulating water circulation process comprises the following steps: circulating water in the water collecting tank 510 is filtered by the circulating water pump 520, enters the heat exchanger 300 along a circulating water pipeline, and then enters the spraying module 540; the sprayed circulating water from the spray module 540 is sprayed on the evaporative cooling heat exchanger 300; the water flowing out of the evaporative cooling heat exchanger 120 flows into the wet film 200 and then flows into the water collection tank 510 to form a cycle.
3) The complete external gas circulation process is as follows: the outside air enters the wet film 200 from the air inlets 710 at the two sides of the equipment for humidification and cooling; the humidified and cooled external air enters the evaporative cooling heat exchanger 120 upwards for evaporation and heat exchange, and then flows through the water receiving module 110 and is sent out through the air outlet 720 by the fan 400.
Compared with the existing closed cooling tower, the embodiment carries out liquid-liquid heat exchange from the circulating water of the water collecting tank on the heat exchanger after the cooling water is indirectly evaporated, so that the cooled fluid of the whole fluid cooling device is greatly enhanced due to the heat exchange capacity between the cooled fluid and the circulating water, the water outlet temperature of the whole fluid cooling device is further reduced, the temperature of the cooled fluid is close to the water inlet temperature of the circulating water entering the heat exchanger, the cooling capacity of the whole device is greatly improved, meanwhile, cold water generated by a wet film is sprayed on the evaporation cooling heat exchanger after being heated, the evaporation capacity of system water can be increased, the effect of increasing the cooling capacity of the cooling device is also achieved, and the cooling efficiency and the cooling capacity of the whole device are greatly improved by organically combining the two.
Further, the evaporative cooling heat exchanger 120 of the present embodiment is preferably a radial finned tube heat exchanger arranged in a V-shape or an inverted V-shape. As shown in fig. 3 and 4, the radial finned tube heat exchanger is composed of a coil 121 and fins 122, the coil 121 is composed of a liquid guide part 121a and a connecting part 121b, the fins on the radial finned tube heat exchanger are uniformly arranged, completely cover and uniformly divide an air circulation space inside the finned tube heat exchanger, and are corrugated in the air flow direction or staggered in the air flow direction; the flow direction of the cooled fluid is arranged in a counter-current manner in the radial finned tube heat exchanger layer relative to the air flow direction.
The liquid guide parts connected in the vertical direction are connected in an S shape through the connecting parts 121b to form a row of vertical coil pipes, so that the cooled fluid in each row of vertical coil pipes is ensured to flow out from top to bottom, the cooled fluid entering the radial finned tubes and the air entering the radial finned tubes are subjected to heat exchange in a countercurrent mode between the whole layers, and the heat exchange efficiency is high.
The fins 122 of the radial finned tube heat exchanger of the embodiment shown in fig. 4 are corrugated in the direction of air flow (not shown in the drawings, and those skilled in the art can deduce corrugated fins from straight finned fins in fig. 3) or are arranged in a staggered manner or in a corrugated staggered manner. The fins of the radial finned tube heat exchanger are corrugated along the airflow direction, so that the contact area of air and the fins is increased and the heat exchange efficiency is improved compared with the conventional straight-sheet-shaped situation. The fins of the radial finned tube heat exchanger are arranged in a staggered mode along the air flow direction, so that air flow disturbance is increased and heat exchange efficiency is improved compared with the conventional arrangement. Particularly, when the fins are arranged in a staggered mode, the fins in one row can extend into the space between the fins in the adjacent row, the area of the whole fins is increased, air flow disturbance is enhanced, and the heat exchange efficiency of the heat exchanger is improved.
Preferably, the indirect evaporative fluid cooling device according to this embodiment is further provided with an inlet air temperature and humidity sensor, an outlet air temperature sensor, an inlet water temperature sensor, an outlet water temperature sensor, and a controller, and the controller can automatically adjust the loads of the fan 400 and the circulating water pump 520 according to the outlet water temperature measured value and the outlet water temperature target value, so that the outlet water temperature reaches a preset value.
Preferably, a hydrophilic coating with an infrared radiation heat dissipation material is arranged on the surface of the evaporative cooling heat exchanger. In this embodiment, the coating contains nano-silica or nano-alumina, and transition metal oxides such as cobalt, nickel, and manganese. The coating can improve the heat exchange efficiency of the evaporative cooling heat exchanger, better adsorbs water drops to form a water film, increases the evaporation efficiency of spray water, and improves the cooling capacity of the indirect evaporative fluid cooling device on the whole.
Preferably, the spraying module 540 is formed by connecting a plurality of nozzles and pipelines, the nozzles are uniformly arranged and aligned with the evaporative cooling heat exchanger, and the average particle size of water drops sprayed by the nozzles is less than 1 mm. The shower nozzle is preferably solid conical nozzle, through preferred shower nozzle and water pressure, makes the shower water be the form of the particle size less than 1mm droplet and evenly sprays on evaporation cooling heat exchanger (preferred average particle size is 0.5 mm's technology), and not traditional rivers column sprays, also not traditional drip, and this kind of spraying makes the drop of shower water evenly distributed on evaporation cooling heat exchanger surface, and makes the shower water be obvious temperature gradient distribution in the air flow direction, and the shower water temperature is high above the evaporation cooling heat exchanger, and the shower water temperature is low below the evaporation cooling heat exchanger. Experiments show that when the particle size of the spray water is less than 0.5mm, most of the spray particles are easily blown away by wind; when the particle size of spraying water is larger than 1mm, the spraying water is unevenly distributed, and meanwhile, the evaporation rate is reduced because the total surface area of the spraying water outlet ball is reduced.
Example two:
as shown in fig. 5, the difference between the second embodiment and the first embodiment is that an air-cooled surface air cooler, an air-cooled circulating pump and a check valve are further added after the cooled fluid flows out of the heat exchanger.
The air-cooled surface air cooler 130 is disposed at a front side or a lower side of the wet film 200 in an air intake direction, and is communicated with the air inlet 710. The water outlet of the air cooling surface cooler 130 is connected with the fluid inlet 810 of the indirect evaporative fluid cooling device through a pipeline; an air cooling circulating pump 140 and a check valve 150 are connected between the water inlet of the air cooling surface cooler 130 and the cooled fluid outlet of the heat exchanger 300 in sequence through pipelines.
When the temperature of a fluid outlet of the whole indirect evaporative fluid cooling device is lower than the temperature of an environment dry bulb, the air cooling surface air cooler precools air entering a wet film by means of cooled fluid lower than the temperature of the environment dry bulb, the wet film is favorably obtained by cold water with lower temperature and cold air with lower temperature, so that the temperature of a water collecting tank of the whole device is lower, the heat exchange between the cooled fluid and circulating water of the whole device is more favorably realized, the temperature of the cooled fluid is reduced to be lower, and the cooling capacity of the whole device is enhanced. Generally, when the air temperature can be reduced by 3-5 ℃ through the optimized air cooling surface air cooler and the direct evaporation efficiency of the wet film reaches more than 95%, the air is pre-cooled through the air cooling surface air cooler, the pre-cooled air is directly evaporated through the wet film, and the air temperature of the wet film and the temperature of the spraying water of the wet film can be reduced to be lower than the temperature of a wet bulb.
It is often the case for the present embodiment to be applied to a data center that the fluid outlet temperature of the entire indirect evaporative fluid cooling device is lower than the ambient dry bulb temperature, which accounts for most of the time of the year.
When the ambient temperature is below the freezing point in winter, the temperature of the fluid outlet is higher than the ambient temperature, and the air heating function can be achieved. The icing in the cooling tower can be prevented, so that the cooling tower can be operated under the severe working condition. For example, when the fluid inlet temperature is 30 ℃, the fluid outlet temperature is 15 ℃ and the ambient temperature is below 0 ℃, cold air outside the device is firstly heated by the fluid above 15 ℃ and then enters the wet film. The air temperature heated by the air surface cooler reaches above the freezing point by optimizing the parameters of the air surface cooler, so that the heated air cannot freeze on the wet film through the wet film. Meanwhile, under the working condition, the air surface cooler also plays a role in cooling the fluid to be cooled while heating the outdoor air, and the cooling capacity of the whole equipment under the working condition is enhanced.
The embodiment adopts the shunted cooled fluid to pre-cool the air, can increase the cooling capacity of the system in the winter dry cooling mode, and can also preheat the air at a lower temperature to prevent the interior from freezing, and also can start the spraying mode in winter to increase the cooling capacity of the system and reduce the power consumption.
Example three and example four
As shown in fig. 6 and 7, the third and fourth embodiments are based on the first and second embodiments and further optimize the water collector to the fluid pre-cooling surface cooler 110a, so that the residual cold in the air is fully utilized to cool the cooled fluid while collecting the water vapor, thereby improving the utilization rate of the residual cold in the air of the cooling tower and improving the cooling capacity of the indirect evaporative fluid cooling device.
Preferably, the surface of the fluid precooling surface cooler is provided with a hydrophilic coating added with an infrared radiation heat dissipation material. In this embodiment, the coating layer contains nano silica or nano alumina, and also contains transition metal oxides such as cobalt, nickel, manganese, and the like. The coating can improve the heat exchange efficiency of the fluid precooling surface air cooler, better adsorb water drops to form a water film, increase the evaporation efficiency of spray water and improve the cooling capacity of the indirect evaporative fluid cooling device on the whole.
The technical features of the above embodiments can be arbitrarily combined, and for the sake of brevity, all possible combinations of the technical features in the above embodiments are not described, but should be considered as the scope of the present specification as long as there is no contradiction between the combinations of the technical features.
The above examples only represent preferred embodiments of the present invention, which are described in more detail and detail, but are not to be construed as limiting the scope of the invention. It should be noted that, for those skilled in the art, without departing from the spirit of the present invention, several variations and modifications can be made, which are within the scope of the present invention. Therefore, the protection scope of the present invention should be subject to the appended claims.
Claims (10)
1. An indirect evaporative fluid cooling device with a built-in heat exchanger is characterized in that:
comprises a shell, an air inlet, an air outlet, a fan, a fluid inlet, a water collecting module, a spraying module, an evaporative cooling heat exchanger, a fluid outlet, a wet film, a heat exchanger, a water collecting tank, a circulating water pump and a water replenishing valve;
the fan is arranged at the upper part of the indirect evaporative fluid cooling device, the water receiving module is arranged below the fan, the evaporative cooling heat exchanger is arranged below the water receiving module, the wet film is arranged below the evaporative cooling heat exchanger, and the wet film is communicated with the air inlet;
the fluid inlet, the evaporative cooling heat exchanger, the heat exchanger and the fluid outlet are connected in sequence through a cooled fluid pipeline;
the spray module is arranged above the evaporative cooling heat exchanger, a plurality of spray heads of the spray module are uniformly distributed above the upper surface of the evaporative cooling heat exchanger, and nozzles of the plurality of spray heads are arranged in alignment with the upper surface of the evaporative cooling heat exchanger;
the water replenishing valve is connected with the water collecting tank; the water collecting tank, the circulating water pump, the heat exchanger and the spraying module are connected through a circulating water pipeline.
2. The indirect evaporative fluid cooling device of claim 1, wherein:
the indirect evaporative fluid cooling device also comprises an air cooling surface air cooler, an air cooling circulating pump and a check valve, wherein the air cooling surface air cooler is arranged on the front side or below the air inlet direction of the wet film, and the air cooling surface air cooler is communicated with the air inlet; the water outlet of the air cooling surface cooler is connected with the fluid inlet of the indirect evaporative fluid cooling device through a pipeline; and a cooled fluid outlet of the fluid cooling heat exchanger and a water inlet of the air cooling surface air cooler are sequentially connected with the air cooling circulating pump and the check valve through pipelines.
3. The indirect evaporative fluid cooling device of claim 1 or 2, wherein:
the evaporative cooling heat exchanger is a radial finned tube heat exchanger, and the radial finned tube heat exchanger is arranged in a V shape or an inverted V shape; fins on the radial finned tube heat exchanger are uniformly distributed, completely cover and uniformly divide an air circulation space inside the finned tube heat exchanger, and are corrugated along the air flow direction or staggered along the air flow direction; the flow direction of the cooled fluid is arranged in a counter-current manner in the radial finned tube heat exchanger layer relative to the air flow direction.
4. The indirect evaporative fluid cooling device of claim 1 or 2, wherein:
the indirect evaporative fluid cooling device is further provided with an air inlet temperature and humidity sensor, an air outlet temperature sensor, an water inlet temperature sensor, a water outlet temperature sensor and a controller, wherein the controller can automatically adjust the load of the fan and the load of the circulating water pump according to the water outlet temperature and a preset temperature target value, so that the water outlet temperature reaches the preset temperature target value.
5. The indirect evaporative fluid cooling device of claim 1 or 2, wherein:
the water receiving module is a fluid precooling surface cooler, and the fluid inlet, the fluid precooling surface cooler, the evaporative cooling heat exchanger and the fluid outlet are sequentially connected through the cooled fluid pipeline.
6. The indirect evaporative fluid cooling device of claim 1 or 2, wherein:
the indirect evaporative fluid cooling device is also provided with an automatic filtering and sewage draining device, and the automatic filtering and sewage draining device is arranged between the circulating water pump and the heat exchanger.
7. The indirect evaporative fluid cooling device of claim 1 or 2, wherein:
the heat exchanger is a plate heat exchanger or a shell and tube heat exchanger.
8. The indirect evaporative fluid cooling device of claim 1 or 2, wherein:
and a hydrophilic coating added with an infrared radiation heat dissipation material is arranged on the surface of the evaporative cooling heat exchanger.
9. The indirect evaporative fluid cooling device of claim 5, wherein:
the surface of the fluid precooling surface cooler is provided with a hydrophilic coating added with an infrared radiation heat dissipation material.
10. The indirect evaporative fluid cooling device of claim 1 or 2, wherein:
the average particle size of water drops sprayed by the spray head of the spray module is less than 1 mm.
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| Application Number | Priority Date | Filing Date | Title |
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| CN202020801064.2U CN212320479U (en) | 2020-05-14 | 2020-05-14 | Indirect evaporative fluid cooling device with built-in heat exchanger |
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| CN202020801064.2U CN212320479U (en) | 2020-05-14 | 2020-05-14 | Indirect evaporative fluid cooling device with built-in heat exchanger |
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| CN212320479U true CN212320479U (en) | 2021-01-08 |
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